|Publication number||US5419890 A|
|Application number||US 08/260,130|
|Publication date||May 30, 1995|
|Filing date||Jun 14, 1994|
|Priority date||Jan 19, 1994|
|Also published as||WO1995034504A1|
|Publication number||08260130, 260130, US 5419890 A, US 5419890A, US-A-5419890, US5419890 A, US5419890A|
|Inventors||M. Yazid Saidi|
|Original Assignee||Valence Technology, Inc.|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (8), Referenced by (52), Classifications (20), Legal Events (6)|
|External Links: USPTO, USPTO Assignment, Espacenet|
This application is a continuation-in-part of United States patent application Ser. No. 08/184,089, filed Jan. 19, 1994, pending; entitled "METHOD OF MAKING V6 O13+x [O(x<x≦2.0]" which application is incorporated herein by reference in its entirety.
The present invention provides a method of synthesizing non-stoichiometric solid vanadium oxide V6 O13+x [0<X≦2.0]. Vanadium oxides are often employed as cathode active materials for use in solid secondary electrochemical cells.
Solid state lithium electrochemical cells are known in the art and typically consist of a lithium or lithium-based metal anode, a lithium-ion conducting solid electrolyte, and a cathode containing a lithium ion insertion electrode material. An insertion electrode material is capable as acting as a cathode by virtue of its ability to reversibly accommodate lithium ions physically inserted into its structure during discharge of the cell and subsequently removed therefrom during charging of the cell. Such insertion electrode materials (or intercalation compounds) include V2 O5, TiS2, V6 O13, LiCoO2 which have satisfactory specific energy densities of about 300-900 Wh kg-1 and mid-discharge voltages of about 2-3 volts.
Like other elements in the transition metal group including niobium and tantalum, vanadium forms numerous and frequently complicated compounds because of its variable valence. The four principle oxidation states of vanadium are 2+, 3+, 4+ and 5+, and it forms derivatives from more or less well defined radicals such as VO2+ and VO3+. However, the vanadium oxide solids possess nominal stoichiometries which indicate a mixture of vanadium oxidation states is present in certain solid phases of vanadium.
Solid lithium electrochemical cells using V6 O13 as the active cathode material are well studied. K. West et al., J. Power Sources, 14 (1985) 235-246, studied V6 O13 as a cathode material for lithium cells using polymeric electrolytes. They found that the lithium insertion reaction was reversible in the composition interval Lix V6 O13 [0≦x≦8]. The high stoichiometric energy density for the ultimate composition Li8 V6 O13, 890 W h/kg, is very favorable for battery applications. P.A. Christian et al., U.S. Pat. No. 4,228,226 suggest that lithiated vanadium oxides of the composition Lix VO2+y [0<y≦0.4] may be prepared chemically by treatment of VO2+y with n-butylithium in hexane. Christian et at. report that the unit cell parameters derived from X-ray powder diffraction data suggests that the compositions Lix V6 O13 have a structure very similar to that of the monoclinic V6 O13 i.e. VO2+y [0.1< y<0.2], prepared at higher temperature. The use of Lix VO2+y, chemically manufactured as aforesaid, as the positive electrode material in a cell, permits the manufacture of cells in the discharged state.
It has been reported in U.S. Pat. No. 4,228,226, the disclosure of which is incorporated herein by reference in its entirety, that vanadium oxides with nominal compositions close to V6 O13 i.e. oxides with the nominal stoichiometry range from VO2.05 to VO2.2 are readily prepared by the thermal decomposition of ammonium vanadate, NH4 VO3, at a controlled rate in an inert atmosphere such as argon or nitrogen, at a temperature of approximately 450° C. Furthermore, the heat treatment of V6 O13 prepared in this manner can alter the lithium capacity of the material when used as a cathode active material in solid secondary lithium cells. It has also been observed that the morphology of vanadium oxide solids can affect the lithium capacity of the material under the same circumstances.
D. W. Murphy et at., J. Electrochemical Soc. 128 (1981) 2053, report the synthesis of V6 O13 and V6 O13+x [0<X≦0.5]. Stoichiometric amounts of V2 O5 and vanadium metal powder were intimately mixed and heated to 600° C. in an evacuated quartz tube. The vanadium-oxygen stoichiometry was verified by TGA in an oxygen atmosphere. V6 O13+x [0<X≦0.5] was produced by ball milling vacuum dried NH4 VO3 and thermally decomposing the ammonium vanadate under an argon stream. The disclosure of D. W. Murphy et al. is incorporated herein by reference in its entirety.
Vanadium oxides V3 O7, V4 O9, V6 O13 and V6 O--+x[0.16≦X≦0.5] have been examined by Murphy et al., ibid., as cathode materials in ambient temperature non-aqueous secondary lithium cells. According to Murphy et al., the best cathode materials are V6 O13 and a slightly oxygen-rich V6 O13+x. Only the latter cathode materials consistently exhibited substantial capacities, good rechargability, and high charge potentials; and therefore made the best candidates for use as cathode active materials in non-aqueous lithium secondary batteries.
A related co-pending application describes the use and method of making V6 O14+x [0<x≦1.0], Ser. No. 08/184,087, filed Jan. 19, 1994, as Attorney Docket No. 1325 (028574-322) entitled "A CATHODE ACTIVE MATERIAL V6 O14+x [0<x≦1.0], AND SOLID SECONDARY LITHIUM CELLS BASED THEREON" which is incorporated herein by reference in its entirety.
The oxidation of V6 O13 in a controlled oxidation atmosphere at high temperature is difficult if the formation of V2 O5 is to be avoided. Oxidation at lower temperatures is preferable but requires the use of an appropriate solvent. Aqueous media can be used but a low boiling organic solvent would make drying the product simpler and be less likely to interfere with the lithium intercalation properties of the product.
It would be advantageous if a low temperature method for making V6 O13+x [0<X≦2.0] in an organic solvent could be found which provides control over the degree of non-stoichiometry in the product compound, i.e. controls the value of X.
The present invention improves the morphology of vanadium oxide having nominal stoichiometry close to V6 O13 by producing V6 O13+x of particle size about 2 to 5 μm before grinding. It also improves the cycle life and lithium capacity of vanadium oxide cathodes while maintaining a crystalline structure similar to that of V6 O13.
In the method of the present invention V6 O13+x [0<X≦2.0] is prepared from V6 O13 in a stirred organic medium contained in a reaction vessel. V6 O13 is slowly contacted with at least a nominal stoichiometric amount of hydrogen peroxide for the reaction:
V6 O13 +XH2 O2 →V6 O13+x +XH2 O
to form the product V6 O13+x. The hydrogen peroxide is normally added slowly over a period of from about 4 to about 12 hours. In a preferred embodiment, a stream of oxygen is added to the stirred organic medium. Preferably, the reaction vessel and its contents are maintained at a temperature in the range of from about 10° C. to about 65° C. To produce a product V6 O13+x of higher oxygen content, the reaction vessel is sealed to maintain constant volume reaction conditions. The product is a micro-crystalline solid which is filtered, washed and dried before further use.
Prior to describing this invention in further detail, the following terms will first be defined.
As used herein, the following terms have the following meanings.
The term "stoichiometric" or "stoichiometric compound" refers to a compound where the ratio of the number of atoms to each other, as determined from atomic weight, is a ratio of small, whole numbers. In "non-stoichiometric compounds" there are defects in the crystal lattice or partial replacement of the atoms of one element by those of another. The term "nominal stoichiometry" is used to refer to non-stoichiometric compounds where the ratio of the number of atoms to each other is not a ratio of small whole numbers.
The term "oxidation state" of an element in a compound refers to the difference between the number of electrons associated with an ion in the compound as compared with the number of electrons associated with the neutral atom of the element. In "oxidation" the oxidation state of an atom is increased. One way to perform oxidation is to increase the proportion of oxygen in the compound.
The term "hydrogen peroxide", H2 O2, refers to a colorless, syrupy liquid prepared by several well known methods. Hydrogen peroxide is soluble in water and the aqueous concentration is often expressed as the volume of O2 that can be liberated e.g. 100 vol. hydrogen peroxide is 30.36% (by vol.) H2 O2 or 27.52% (by wt) H2 O2.
The term "organic medium" as used herein refers to an organic solvent and an organic carrier of dispersed particles. That is, a solvent whose principal atomic constituents are carbon and hydrogen. The solvent is preferably a polar solvent boiling below about 80° C. Polar solvents are those containing at least one hetero atom, such as oxygen and nitrogen. It is required that the solvent be miscible, nonreactive and compatible with hydrogen peroxide. Preferably, the solvent is easily removed from the product by ordinary drying procedures.
The term "electrochemical cell" or "electrolytic cell" refers to a composite structure containing a positive electrode, a negative electrode and a ion-conducting electrolyte interposed therebetween.
The term "capacity" or "discharge capacity" of the cell refers to the total amount of charge the fully charged battery can discharge to a certain final cell voltage. It is measured in ampere-hours. It is a measure of the useful charge in the battery. The initial capacity is that measured during the first full cycle of the cell. A comparison of the average cycle capacity to that of the initial cycle provides a measure of how well the cell maintains a constant capacity over repeated cycles.
The term "cycle" refers to a consecutive charge/discharge cycle. The ability of the cell or battery to maintain a useful capacity for many cycles indicates the useful life of the cell or battery.
The terms "solid, single-phase polymeric electrolyte" and "solid polymeric electrolyte" refer to an ionically conducting polymeric solid, normally comprising an inorganic salt, a compatible electrolyte solvent, and a solid polymeric matrix.
The term "solid polymeric matrix", as used herein, refers to a polymer made by polymerizing or copolymerizing monomer(s) or prepolymer(s) or oligomer(s). Certain solid polymeric matrices are useful in the preparation of solid polymeric electrolytes, are well known in the art, and are described, for example, in U.S. Pat. Nos. 4,908,283 and 4,925,751, both of which are incorporated herein by reference in their entirety.
The term, "a solid polymeric matrix forming monomer or polymer precursor" refers to inorganic or organic materials which in monomeric, oligomeric or polymeric form can be polymerized, or further polymerized, as by cross-linking, preferably in the presence of a salt and a solvent, to form solid polymeric matrices which are suitable for use in solid polymeric electrolytes in electrochemical cells. Typically, the solid polymeric matrix forming monomer or polymer precursor has at least one heteroatom capable of forming donor-acceptor bonds with inorganic cations, e.g. alkali ions.
The term "compatible electrolyte solvent", or in the context of components of the solid electrolyte, just "solvent", refers to a low molecular weight organic plasticizer added to the electrolyte and/or the cathode composition, which may also serve the purpose of solubilizing the inorganic ion salt. The solvent is any compatible, relatively non-volatile, aprotic, relatively polar, solvent. Preferably, these materials have boiling points greater than about 80° C. to simplify manufacture and increase the shelf life of the electrolyte/battery. Typical examples of solvent are mixtures of such materials as propylene carbonate, ethylene carbonate, gamma-butyrolactone, tetrahydrofuran, glyme, diglyme, triglyme, tetraglyme, dimethylsulfoxide, dioxolane, sulfolane, and the like. A particularly preferred solvent is disclosed in U.S. Patent Application Ser. No. 07/918,438, filed Jul. 22, 1992, which application is incorporated herein by reference in its entirety.
The term "salt" refers to any salt, for example, an inorganic salt, which is suitable for use in a solid electrolyte. Representative examples of suitable inorganic ion salts are alkali metal salts of less mobile anions of weak bases having a large anionic radius. Examples of such anions are I-, Br-, SCN-, ClO- 4, BF- 4, PF- 6, AsF+ 6, CF3 COO+, CF3 SO- 3, and the like. Specific examples of suitable inorganic ion salts include LiClO4, LiI LiSCN, LiBF4, LiAsF6, LiCF3 SO3, LiPF6, NaI, NaSCN, KI, and the like. The inorganic ion salt preferably contains at least one atom selected from the group consisting of Li, Na and K.
The term "electrochemical cell" refers to a composite structure containing an anode, a cathode, and an ion-conducting electrolyte interposed therebetween.
The "anode" refers to an electrode for the half-cell reaction of oxidation on discharge, which is typically comprised of a compatible anodic material, i.e. any material which functions as an anode in the solid electrochemical cell. Such compatible anodic materials are well known in the art and include, by way of example, lithium, lithium alloys, such as alloys of lithium with aluminum, mercury, iron, zinc and the like, and intercalation-based anodes such as carbon, tungsten oxide and the like.
The "cathode" refers to the counter-electrode to the anode and is typically composed of a compatible cathodic material (i.e. insertion compounds) which is any material which functions as a cathode in an electrochemical cell. Such compatible cathodic materials are well known to the art and include by way of example, manganese oxides, molybdenum oxides, vanadium oxides, such as V6 O13, sulfides of molybdenum, titanium and niobium, lithiated cobalt oxides, lithiated manganese oxides, lithiated nickel oxides, chromium oxides, copper oxides, and the like. The particular compatible cathodic material employed is not critical.
V6 O13 has been prepared by the reaction of stoichiometric amounts of V2 O5 and vanadium metal powder intimately mixed and heated to 600° C. in an evacuated quartz tube. After one day, the temperature was increased to 680° C. for 1-3 days. The resulting micro-crystalline product was deep purple in color and exhibited a metallic luster (see Murphy et al. ibid). This product typically has an stoichiometric formula of about V6 O12.9 to V6 O13.1 and is referred to in the art as V6 O13.
V6 O13 and vanadium oxides with nominal compositions close to V6 O13 have been prepared by the thermal decomposition of ammonium vanadate (NH4 VO3) at a controlled rate in an inert atmosphere (such as argon or nitrogen) or in a reducing atmosphere (such as H2, NH3 or SO2) at a temperature of approximately 450° C. (see U.S. Pat. No. 4,228,226). The preparation and analysis of V6 O13 powders has also been described by K. West et al., Electrochim. Acta, 28 (1983) 1829, the disclosure of which is incorporated herein by reference in its entirety. The V6 O13 used in the examples was obtained from CERAC, Inc., Milwaukee, Wis.
Prior to dispersion of the V6 O13 in an organic medium, the V6 O13 solid is preferably ground to a fine powder. The powder is dispersed in the reaction vessel containing the organic medium by a rapid stirring means. An aqueous solution of H2 O2 is then added very slowly to the stirred V6 O13 which is preferably maintained at a temperature near room temperature. The temperature of the reaction vessel can range from about 10° C. to about 45° C. The concentration of added aqueous H2 O2 is in the range of from about 10% (by vol) to 80% (by vol), preferably from 20% to 60% and most preferably about 30% relative to the organic medium.
A stream of oxygen gas can also be added to the stirred organic reaction mixture during the course of the reaction, i.e. during the 4 to 12 hours it requires to slowly add a nominally stoichiometric amount of H2 O2. To produce a product V6 O13+x of higher oxygen content, the reaction vessel may be sealed to maintain constant volume reaction conditions. The slow addition of H2 O2 to the stirred organic reaction mixture preferably involves the addition of no more than about 5 milligrams of H2 O2 per gram of V6 O13 per minute.
The product of the reaction is a micro-crystalline solid which is filtered from the organic medium, washed with distilled water, and dried in a air-blown oven at about 60° C. The micro-crystalline mass may be crushed and the balance of the solvent removed by drying the crushed mass in vacuo.
Analysis is made gravimetrically by weighing the product as the pentoxide. Specifically, TGA (600° C) is used in the reaction V6 O13+x +(1-1/2X)O2 →3V2 O5, to determine X by weight increase. X was also determined by potentiometfic titration with KMn O4. The reaction methods of the present invention have been found to provide several means of controlling the non-stoichiometric parameter X in the product V6 O13+x. Such means include the rate of addition of H2 O2, the concentration of H2 O2, the addition of O2, the temperature, and the use of a constant volume reaction. In general, to increase the value of X a slower rate of addition of more concentrated H2 O2 is used, O2 is added, the temperature is maintained near room temperature, and a constant volume reaction is used. One or more of these means can be used simultaneously to achieve the stated objective. The following examples are illustrative.
10 grams of V6 O13 were thoroughly dispersed in 12.5 ml of acetone for about 15 minutes using a magnetic stirrer. The speed was such as not to allow the powder to settle down the beaker. Then 10.8 mls of a 30% aqueous solution of H2 O2 was added slowly, typically one drop every few seconds (100-200 μls every 5 seconds). Depending upon the initial composition of the vanadium oxide, the total amount of reactant added contained between about 5-10% excess hydrogen peroxide to drive the reaction to completion. After addition of the H2 O2 was completed, the mixture was stirred for from 4-6 hours. The mixture is dried in an airblown oven at 60° C. to make it easier to crush the powder and to remove the balance of the solvent. The powder is dried in vacuo at a conveniently higher temperature of about 150° C.
300 grams of V6 O13 were thoroughly dispersed in 500 mls of acetone using a high torque mixer (Lightnin L5U8f). The speed was adjusted to 250 rotations per minute. This was sufficient to prevent the mixture from settling down a custom made reaction chamber. Then 69.4 mls of a 30% solution of hydrogen peroxide was slowly added (typically about 100 to 200 μl every 5 seconds). The amount of reactant added contained between 5 to 10% excess peroxide to drive the reaction to completion. After addition of the reactant was completed, the mixture was left to stir for 4 to 6 hours. The mixture was then dried in an airblown oven in the manner described above.
The following prophetic examples further illustrate the methods described herein.
V6 O13 +XH2 O2 .increment.V6 O13+x +XH2 O
10 grams of V6 O13 is dispersed in 10 ml of acetone for about 10 minutes. 2 ml of H2 O2 (30%, by vol, aqueous solution) is slowly added to the cooled mixture of V6 O13 in acetone at a rate of about one drop every ten seconds, while the mixture is continually stirred. After addition of the H2 O2 is completed, the mixture is stirred for from 4-6 hours. The mixture is dried in an airblown oven at 60° C. to make it easier to crush the powder and to remove the balance of the solvent. The powder is dried in vacuo at a conveniently higher temperature of about 150° C.
As described in Example 3, nominal stoichiometric amounts of V6 O13 and H2 O2 (X=1) iS mixed in acetonitrile with a stream of oxygen applied at the rate of 25 cc/min for 12 hours. The resulting material is filtered and washed with water, predried at 65° C, and then dried under vacuum at 150° C.
In the examples set forth above, other solvents can be used in place of acetone and acetonitrile as exemplified above merely by substitution. Such other solvents include, by way of example, methanol, tetrahydrofuran, N-methyl pyrollidone, and the like.
It is contemplated that the use of such organic solvents instead of water in these examples will provide benefits insofar as these low boiling solvents can be easily evaporated without applying severe heating conditions. Also, certain low boiling organic solvents can resist oxidation thereby providing some of the same benefits as water. Additionally, such solvents also provide for efficient removal from the final product as compared to water which in most cases ends up tightly adsorbed to the vanadium oxide surface and can only be removed by prolonged heating which can have adverse effects on the final performance of the vanadium oxide.
The vanadium oxide cathode mixtures described herein are useful in preparing electrochemical cells having improved cumulative capacity and cycle life in comparison to electrochemical cells containing conventional vanadium oxide cathode formulations. Moreover, the subject vanadium oxide cathode mixtures should be particularly useful in preparing solid electrolyte cells having improved cumulative capacity and cycle life in comparison to solid electrolyte cells comprising conventional vanadium oxide cathode compositions.
The following hypothetical example is offered to illustrate the preparation of electrolytic cells using a vanadium oxides prepared in the methods described herein and should not be construed in any way as limiting its scope.
A solid electrolytic cell is prepared by first preparing a cathodic paste which is spread onto a current collector. An electrolyte solution is then placed onto the cathode surface and the cathode paste and electrolyte solution are simultaneously cured to provide for the solid electrolyte composition. Then, the anode is laminated onto the solid electrolyte composition to provide for a solid electrolytic cell. The specifics of this construction are as follows:
A. The Current Collector
The current collector employed is a sheet of aluminum foil having a layer of adhesion promoter attached to the surface of the foil which will contact the cathode so as to form a composite having a sheet of aluminum foil, a cathode and a layer of adhesion promoter interposed therebetween. The aluminum foil is preferably an alloy that is identified by either the industry specifications 1235-H19 (99.35% min. Al), or 1145-H19 (99.45% min. Al), and which is available from All Foils, Inc., Brooklyn Heights, Ohio.
The adhesion promoter layer is prepared as a dispersed colloidal solution in one of two methods. The first preparation of this colloidal solution for this example is as follows:
84.4 parts by weight of carbon powder (Shawinigan Black®--available from Chevron Chemical Company, San Ramon, Calif.)
337.6 parts by weight of a 25 weight percent solution of polyacrylic acid (a reported average molecular weight of about 90,000, commercially available from Aldrich Chemical Company--contains about 84.4 grams polyacrylic acid and 253.2 grams water)
578.0 parts by weight of isopropanol
In a preferred embodiment of the first method, an additional amount of water, e.g., 2-3 weight percent water based on the total weight of the colloidal solution, is incorporated to enhance coatability. Also, about 1 weight percent methyl ethyl ketone is added to the composition to enhance wettability of the aluminum.
The carbon powder and isopropanol are combined with mixing in a conventional high shear colloid mill mixer (Ebenbach-type colloid mill) until the carbon is uniformly dispersed and the carbon particle size is smaller than 10 microns. At this point, the 25 weight percent solution of polyacrylic acid is added to the mixer and further mixed for approximately 15 minutes. The resulting mixture is pumped to the coating head and applied by a reverse Gravure roller onto a sheet of aluminum foil (about 9 inches wide and about 0.0005 to about 0.001 inches thick). After application, the solvent is evaporated by placing the mixture/foil into a conventional oven. After evaporation, an electrically-conducting adhesion-promoter layer of about 4-6 microns in thickness is formed. The aluminum foil is then cut to about 8 inches wide by removing approximately 1/2 inch from the sides with a conventional slitter so as to remove any uneven edges; the foil can then be further cut to the desired size.
The second preparation of this colloidal solution comprises mixing 25 lbs of carbon powder (Shawinigan Black®--available from Chevron Chemical Company, San Ramon, CA) with 100 lbs of a 25 weight percent solution of polyacrylic acid (average molecular weight of about 240,000, commercially available from BF Goodrich, Cleveland, Ohio, as Good-Rite K702--contains about 25 lbs polyacrylic acid and 75 lbs water) and with 18.5 lbs of isopropanol. Stirring is done in a 30 gallon polyethylene drum with a gear-motor mixer (e.g., Lighting Labmaster Mixer, model XJ-43, available from Cole-Parmer Instruments Co., Niles, Ill.) at 720 rpm with two 5 inch diameter A310-type propellers mounted on a single shaft. This wets down the carbon and eliminates any further dust problem. The resulting weight of the mixture is 143.5 lbs and contains some "lumps".
The mixture is then further mixed with an ink mill which consists of three steel rollers almost in contact with each other, turning at 275, 300, and 325 rpms respectively. This high shear operation allows particles that are sufficiently small to pass directly through the rollers. Those that do not pass through the rollers continue to mix in the ink mill until they are small enough to pass through these rollers. When the mixing is complete, the carbon powder is completely dispersed. A Hegman fineness of grind gauge (available from Paul N. Gardner Co., Pompano Beach, Fla.) indicates that the particles are 4-6 microns with the occasional 12.5 micron particles. The mixture can be stored for well over 1 month without the carbon settling out or reagglomerating.
When this composition is to be used to coat the current collector, an additional 55.5 lbs of isopropanol is mixed into the composition working with 5 gallon batches in a plastic pail using an air powered shaft mixer (Dayton model 42231 available from Granger Supply Co., San Jose, CA) with a 4 inch diameter Jiffy-Mixer brand impeller (such as an impeller available as Catalog No. G-04541-20 from Cole Parmer Instrument Co., Niles, Ill.). Then, it is gear pumped through a 25 microns cloth filter (e.g., So-Clean Filter Systems, American Felt and Filter Company, Newburgh, N.Y.) and coated as described above.
B. The Cathode
The cathode is prepared from a cathodic paste which, in turn, is prepared from a cathode powder as follows:
i. Cathode Powder
The cathode powder is prepared by combining 94.1±1.1 weight percent V6 O13+x [prepared by the methods described herein] and 5.9±1.1 weight percent of carbon (available from AKZO Chemicals, Inc., Chicago, Ill., under the tradename of Ketjen Black EC 600JD®). About 100 grams of the resulting mixture is placed into a grinding machine (Attritor Model S-1 available from Union Process, Akron, Ohio) and ground for 30 minutes starting at 150 rpm and adjusted to about 250 rpm approximately 10 seconds later and held at that speed for the remainder of the 30 minute duration. Afterwards, the resulting mixture is passed through a 200 mesh screen and then dried in a vacuum or in an inert gas atmosphere (e.g., argon) to produce a cathode powder with a water content of less than about 1000 ppm and preferably less than about 700 ppm.
ii. Cathode Paste
A cathode paste is prepared by combining sufficient cathode powder to provide for a final product having about 53 weight percent V6 O13+x. The paste contains the following (in approximate weight percent):
______________________________________V6 O13+x 53%Carbon 3.7%4:1 propylene carbonate/tri- 31.9%glymepolyethylene oxide 2%polyethylene glycol 8%diacrylateethoxylated trimethylol- 1.4%propane triacrylate______________________________________
The method of preparing 100 grams of the cathode paste is as follows:
31.9 grams of a solvent having a 4:1 weight ratio of propylene carbonate: triglyme is mixed with 8 grams of polyethylene glycol diacrylate (molecular weight about 400 available as SR-344 from Sartomer Company, Inc., Exton, Pa.) and 1.4 grams of ethoxylated trimethylol-propane triacrylate (TMPEOTA) (molecular weight about 450 and available as SR-454 from Sartomer Co., Inc.) in a double planetary mixer (Ross No. 2 mixer, available from Charles Ross & Sons, Co., Hauppage, NY) to form a solvent solution.
53 grams of V6 O13+x, 3.7 grams of carbon, and 2 grams of polyethylene oxide are mixed in a V-blender before being transferred to the double planetary mixer where the blend is stirred at 7.5 Hz and 25° C. (The polyethylene oxide preferably is vacuum dried at 350° C. for three hours prior to use.) The above solvent solution is first passed through 4A molecular sieves and then added to the V6 O13+x and carbon blend under vacuum mixing over a 5 minute period. Afterwards, the mixing speed is increased from 7.5 to 20 Hz and maintained for another 5 minutes. Thereafter, the temperature of the mixture is gradually raised to 85 ° C. over about a 45 minute period and maintained at the elevated temperature for about 30 minutes. Next, the mixing speed is decreased to about 1 Hz and subsequently the temperature of the mixture is allowed to decrease gradually to about 45° C. over about a 30 minute period. Finally, the mixture is mixed for 5 minutes at this temperature.
The resulting cathode paste is maintained at about 45 ° C. until applied onto the current collector. The so-prepared cathode paste can be placed onto the adhesion layer of the current collector by extrusion at a temperature of from about 45° to about 48° C. The extruded cathode past is then spread to a substantially uniform thickness of about 50-120 microns over the current collector by a comma bar.
60.19 grams of propylene carbonate, 15.05 grams of triglyme, and 11.93 grams of urethane acrylate (Actilane SPO23, available from Akcros Chemicals, Ltd., Manchester, United Kingdom) are combined at room temperature until homogeneous. The resulting solution is optionally passed through a column of 4A molecular sieves to remove water and then mixed at room temperature until homogeneous.
At this point, 3 grams of polyethylene oxide film forming agent having a number average molecular weight of about 600,000 (available as Polyox WSR-205 from Union Carbide Chemicals and Plastics, Danbury, Conn.) is added to the solution and then dispersed while stirring with a magnetic stirrer over a period of about 120 minutes. After dispersion, the solution is heated to between 60° C. and 65° C. with stirring until the film forming agent is dissolved. A thermocouple is placed at the edge of the vortex created by the magnetic stirrer to monitor solution temperature. The solution is cooled to a temperature of less than 48° C. and then 9.83 grams of LiPF6 are added to the solution over a 120 minute period while thoroughly mixing to ensure a substantially uniform temperature profile throughout the solution. Cooling is applied as necessary to maintain the temperature of the solution between 45° and 48° C.
In one optional embodiment, the polyethylene oxide film forming agent is added to the solution via a mini-sieve such as a 25 mesh mini-sieve commercially available as Order No. 57333-965 from VWR Scientific, San Francisco, Calif.
The resulting solution contains the following:
______________________________________Component Amount Weight Percenta______________________________________Propylene Carbonate 60.19 g 60.19Triglyme 15.05 g 15.05Urethane Acrylate 11.93 g 11.93LiPF6 9.83 g 9.83PEO Film Forming 3.00 g 3.00AgentTotal 100 g 100______________________________________ a weight percent based on the total weight of the electrolyte solution (100 g)
This solution is then degassed to provide for an electrolyte solution wherein little, if any, of the LiPF6 salt decomposes.
Optionally, the above solution which contains the prepolymer, the polyalkylene oxide film forming agent, the electrolytic solvent and the LiPF6 salt, is filtered to remove any solid particles or gels remaining in the solution. One suitable filter device is a sintered stainless steel screen having a pore size between 1 and 50 microns at 100% efficiency.
In the alternative embodiment, the electrolyte is prepared by the following steps using the same above described electrolyte components:
1. Check the moisture level of the urethane acrylate. If the moisture level is less than 100 ppm water, proceed to step 2. If not, then first dissolve the urethane acrylate at room temperature, <30° C, in the propylene carbonate and triglyme and dry the solution over 4A molecular sieves (Grade 514, 8-12 Mesh from Schoofs Inc., Moraga, CA) and then proceed to step 4.
2. Dry the propylene carbonate and triglyme over 4A molecular sieves (Grade 514, 8-12 Mesh from Schoofs Inc., Moraga, Calif.).
3. At room temperature, <30° C., add the urethane acrylate to the solvent prepared in step 2. Stir at 300 rpm until the resin is completely dissolved. The solution should be clear and colorless.
4. Dry and then sift the polyethylene oxide film forming agent through a 25 mesh mini-sieve commercially available as Order No. 57333-965 from VWR Scientific, San Francisco, Calif. While stirring at 300 rpm, add the dried and pre-sifted polyethylene oxide film forming agent slowly to the solution. The polyethylene oxide film forming agent should be sifted into the center of the vortex formed by the stirring means over a 30 minute period. Addition of the polyethylene oxide film forming agent should be dispersive and, during addition, the temperature should be maintained at room temperature (<30° C.).
5. After final addition of the polyethylene oxide film forming agent, stir an additional 30 minutes to ensure that the film forming agent is substantially dispersed.
6. Heat the mixture to 68° C. to 75° C. and stir until the film forming agent has melted and the solution has become transparent and is light yellow in color. Optionally, in this step, the mixture is heated to 65° C. to 68° C.
7. Cool the solution produced in step 6 and when the temperature of the solution reaches 40° C., add the LiPF6 salt very slowly making sure that the maximum temperature does not exceed 55° C. and preferably does not exceed about 40° C.
8. After the final addition of the LiPF6 salt, stir for an additional 30 minutes, degas, and let sit overnight and cool.
9. Filter the solution through a sintered stainless steel screen having a pore size between 1 and 50 microns at 100% efficiency.
At all times, the temperature of the solution should be monitored with a thermocouple which should be placed in the vortex formed by the mixer.
Afterwards, the electrolyte mixture is then coated by a slot die coater to a thickness of about 25-50 microns onto the surface of the extruded cathode paste prepared as above. The electrolyte and cathode paste are then simultaneously cured by continuously passing the sheet through an electron beam apparatus (available as a Broad Beam electron beam processor from RPC Industries, Hayward, Calif.) at a voltage of about 250 kV and a current of about 48 mA and at a conveyor speed of 50 ft/minute. After curing, a composite is recovered which contains a solid electrolyte laminated to a solid cathode which is affixed to a current collector.
The anode comprises a sheet of lithium foil (about 50 μm thick) which is commercially available from FMC Corporation Lithium Division, Bessemer City, N.C.
E. The Solid Electrolytic Cell
A sheet comprising a solid battery is prepared by laminating the lithium foil anode to the surface of the electrolyte of the above described electrolyte/cathode composite. Lamination is accomplished by minimal pressure.
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US2784075 *||Jun 5, 1952||Mar 5, 1957||Bauerle Lester C||Method of recovering vanadium from leach liquors|
|US3087786 *||May 10, 1960||Apr 30, 1963||Union Carbide Corp||Preparation of high purity vanadium pentoxide from oxidic vanadium materials|
|US3483110 *||May 19, 1967||Dec 9, 1969||Bell Telephone Labor Inc||Preparation of thin films of vanadium dioxide|
|US3728442 *||Jun 7, 1971||Apr 17, 1973||Arkhipov S||Method of producing vanadium pentoxide|
|US4039582 *||Aug 23, 1976||Aug 2, 1977||Gakif Zakirovich Nasyrov||Method of preparing vanadium pentoxide|
|US4119707 *||Mar 7, 1977||Oct 10, 1978||Vereinigte Aluminum-Werke Aktiengesellschaft||Process and equipment for manufacturing vanadium pentoxide|
|US4952467 *||May 19, 1989||Aug 28, 1990||Societe Anonyme Dite: Saft||Process for preparing a compound using a vanadium oxide derivative for the cathode of a thermal cell|
|US5258245 *||Jun 26, 1992||Nov 2, 1993||Matsushita Electric Industrial Co., Ltd.||Lithium rechargeable battery and method of making the same|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US5851696 *||Jan 29, 1996||Dec 22, 1998||Valence Technology, Inc.||Rechargeable lithium battery|
|US5916628 *||Nov 26, 1996||Jun 29, 1999||Matsushita Electric Industrial Co., Ltd.||Method for manufacturing a cell electrode|
|US7313541||Mar 26, 2001||Dec 25, 2007||Jpmorgan Chase Bank, N.A.||System and method for estimating conduit liquidity requirements in asset backed commercial paper|
|US7392210||Aug 3, 2000||Jun 24, 2008||Jpmorgan Chase Bank, N.A.||Workflow management system and method|
|US7392212||Sep 24, 2001||Jun 24, 2008||Jpmorgan Chase Bank, N.A.||User-interactive financial vehicle performance prediction, trading and training system and methods|
|US7567928||Jan 31, 2006||Jul 28, 2009||Jpmorgan Chase Bank, N.A.||Total fair value swap|
|US7593876||Dec 18, 2003||Sep 22, 2009||Jp Morgan Chase Bank||System and method for processing partially unstructured data|
|US7596526||Apr 16, 2002||Sep 29, 2009||Jpmorgan Chase Bank, N.A.||System and method for managing a series of overnight financing trades|
|US7620578||May 1, 2006||Nov 17, 2009||Jpmorgan Chase Bank, N.A.||Volatility derivative financial product|
|US7634435||Aug 8, 2003||Dec 15, 2009||Jp Morgan Chase Bank||Diversified fixed income product and method for creating and marketing same|
|US7647268||May 4, 2006||Jan 12, 2010||Jpmorgan Chase Bank, N.A.||System and method for implementing a recurrent bidding process|
|US7680731||Jun 27, 2007||Mar 16, 2010||Jpmorgan Chase Bank, N.A.||System and method for executing deposit transactions over the internet|
|US7680732||Jul 12, 2007||Mar 16, 2010||Jpmorgan Chase Bank, N.A.||System and method for executing deposit transactions over the internet|
|US7716107||Feb 28, 2008||May 11, 2010||Jpmorgan Chase Bank, N.A.||Earnings derivative financial product|
|US7718319||Sep 25, 2007||May 18, 2010||Board Of Regents, The University Of Texas System||Cation-substituted spinel oxide and oxyfluoride cathodes for lithium ion batteries|
|US7770184||May 21, 2004||Aug 3, 2010||Jp Morgan Chase Bank||Integrated trading platform architecture|
|US7818238||Oct 11, 2005||Oct 19, 2010||Jpmorgan Chase Bank, N.A.||Upside forward with early funding provision|
|US7822682||Apr 19, 2006||Oct 26, 2010||Jpmorgan Chase Bank, N.A.||System and method for enhancing supply chain transactions|
|US7827096||Nov 5, 2007||Nov 2, 2010||Jp Morgan Chase Bank, N.A.||Special maturity ASR recalculated timing|
|US7890407||Oct 30, 2007||Feb 15, 2011||Jpmorgan Chase Bank, N.A.||System and method for estimating conduit liquidity requirements in asset backed commercial paper|
|US7966234||Dec 22, 1999||Jun 21, 2011||Jpmorgan Chase Bank. N.A.||Structured finance performance analytics system|
|US7970688||Jan 15, 2004||Jun 28, 2011||Jp Morgan Chase Bank||Method for pricing a trade|
|US8090639||Jan 29, 2010||Jan 3, 2012||Jpmorgan Chase Bank, N.A.||Method and system for creating and marketing employee stock option mirror image warrants|
|US8280794||Feb 3, 2006||Oct 2, 2012||Jpmorgan Chase Bank, National Association||Price earnings derivative financial product|
|US8352354||Jul 16, 2010||Jan 8, 2013||Jpmorgan Chase Bank, N.A.||System and method for optimizing order execution|
|US8412607||Aug 14, 2012||Apr 2, 2013||Jpmorgan Chase Bank, National Association||Price earnings derivative financial product|
|US8423447||Nov 23, 2004||Apr 16, 2013||Jp Morgan Chase Bank||System and method for allocating nominal and cash amounts to trades in a netted trade|
|US8548886||Apr 26, 2012||Oct 1, 2013||Jpmorgan Chase Bank, N.A.||Account opening system, method and computer program product|
|US8650112||May 23, 2011||Feb 11, 2014||Jpmorgan Chase Bank, N.A.||Total Fair Value Swap|
|US8688569||Mar 23, 2005||Apr 1, 2014||Jpmorgan Chase Bank, N.A.||System and method for post closing and custody services|
|US8722246||Apr 1, 2010||May 13, 2014||Board Of Regents Of The University Of Texas System||Cation-substituted spinel oxide and oxyfluoride cathodes for lithium ion batteries|
|US8738514||Feb 18, 2011||May 27, 2014||Jpmorgan Chase Bank, N.A.||System and method for providing borrow coverage services to short sell securities|
|US20020107784 *||Sep 24, 2001||Aug 8, 2002||Peter Hancock||User-interactive financial vehicle performance prediction, trading and training system and methods|
|US20020188553 *||Apr 16, 2002||Dec 12, 2002||Blauvelt Joseph P.||System and method for managing a series of overnight financing trades|
|US20040148247 *||Apr 14, 2003||Jul 29, 2004||Lawrence Miller||Network-based systems, methods, and software for initiating or executing financial transactions|
|US20040230507 *||Aug 8, 2003||Nov 18, 2004||Jeffrey Davidovitch||Diversified fixed income product and method for creating and marketing same|
|US20050015324 *||Dec 5, 2003||Jan 20, 2005||Jacob Mathews||Systems and methods for trading financial instruments across different types of trading platforms|
|US20050027658 *||Jan 15, 2004||Feb 3, 2005||Moore Stephen G.||Method for pricing a trade|
|US20050060256 *||Jul 2, 2004||Mar 17, 2005||Andrew Peterson||Foreign exchange trading interface|
|US20050188378 *||May 21, 2004||Aug 25, 2005||Miller Lawrence R.||Integrated trading platform architecture|
|US20050222937 *||Mar 31, 2004||Oct 6, 2005||Coad Edward J||Automated customer exchange|
|US20050222938 *||Nov 23, 2004||Oct 6, 2005||Treacy Paul A||System and method for allocating nominal and cash amounts to trades in a netted trade|
|US20050251478 *||Sep 23, 2004||Nov 10, 2005||Aura Yanavi||Investment and method for hedging operational risk associated with business events of another|
|US20080086404 *||Oct 30, 2007||Apr 10, 2008||Jp Morgan Chase Bank, Na||System and method for estimating conduit liquidity requirements in asset backed commercial paper|
|US20090132428 *||Nov 15, 2005||May 21, 2009||Stephen Jeffrey Wolf||Method for creating and marketing a modifiable debt product|
|US20090164384 *||Feb 9, 2005||Jun 25, 2009||Hellen Patrick J||Investment structure and method for reducing risk associated with withdrawals from an investment|
|US20090187512 *||May 31, 2005||Jul 23, 2009||Jp Morgan Chase Bank||Asset-backed investment instrument and related methods|
|US20100138332 *||Jan 29, 2010||Jun 3, 2010||Seaman David A||Method and system for creating and marketing employee stock option mirror image warrants|
|US20110035306 *||Oct 7, 2005||Feb 10, 2011||Jpmorgan Chase Bank, N.A.||System and method for buying and selling securities|
|US20110055113 *||Mar 26, 2010||Mar 3, 2011||Conor Cunningham||Method and system for managing spread orders|
|US20110202452 *||Feb 18, 2011||Aug 18, 2011||Jp Morgan Chase Bank, N.A.||System and method for providing borrow coverage services to short sell securities|
|WO2006066470A1 *||Apr 8, 2005||Jun 29, 2006||Institute Of Physics, Chinese Academy Of Sciences||A lithium iron phosphate positive electrode material having oxygen vacancy for secondary lithium battery and use of the same|
|U.S. Classification||423/594.17, 429/231.5|
|International Classification||H01M10/36, H01M10/0565, H01M10/052, C01G31/02, H01M4/48, H01M4/485, H01M4/131|
|Cooperative Classification||C01P2004/03, H01M10/0565, H01M4/485, H01M10/052, C01G31/02, C01P2002/72, C01P2004/61, H01M4/131, H01M4/661|
|European Classification||C01G31/02, H01M4/485|
|Jun 14, 1994||AS||Assignment|
Owner name: VALENCE TECHNOLOGY, INC., CALIFORNIA
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:SAIDI, M. YAZID;REEL/FRAME:007049/0341
Effective date: 19940614
|Aug 17, 1998||AS||Assignment|
Owner name: DELPHI ENERGY AND ENGINE MANAGEMENT SYSTEMS GROUP
Free format text: LICENSE;ASSIGNORS:VALENCE TECHNOLOGY INC.;VALENCE TECHNOLOGY CAYMAN ISLANDS INC.;REEL/FRAME:009386/0940;SIGNING DATES FROM 19910522 TO 19940912
|Nov 24, 1998||FPAY||Fee payment|
Year of fee payment: 4
|Dec 18, 2002||REMI||Maintenance fee reminder mailed|
|May 30, 2003||LAPS||Lapse for failure to pay maintenance fees|
|Jul 29, 2003||FP||Expired due to failure to pay maintenance fee|
Effective date: 20030530